Investigation of Pool Boiling Heat Transfer from Rough Surface and Microchannel Geometry Under Variable Heat Supply
Date
2019
Authors
Ashok, Walunj Avdhoot.
Journal Title
Journal ISSN
Volume Title
Publisher
National Institute of Technology Karnataka, Surathkal
Abstract
Enormous amount of heat is generated in the Economic Simplified Boiling Water
Reactor (ESBWR) due to exponential heat generation from the fuel rod. A core melt
accident occurs when the heat generated in the nuclear reactor exceeds the heat removed
by the coolant to the point where at least one nuclear fuel element exceeds its melting
point temperature. Critical Heat Flux (CHF) is the phase of boiling after which heat
transfer coefficient drops resulting in the rapid increase in temperature of core. Hence,
understanding the mechanism of CHF is important to control loss of coolant accident
(LOCA). CHF enhancement may retard the LOCA in ESBWR. Passive enhancement
techniques are the most suitable for the nuclear reactor application. In view of the facts
discussed above, the CHF enhancement by two passive techniques namely, rough
surfaces and microchannel geometries is investigated. The transient CHF enhancement
is compared with the steady-state CHF upto 10 bar pressure.
The experimental setup is designed to study the pool boiling of water at 1 bar, 5 bar and
10 bar pressures. The pool boiling experiments are conducted on the thick copper
sample of 20 mm diameter at saturated condition of distilled water. The unidirectional
scratches are made on the sample to obtain wide range of surface roughness varying
from Ra=0.106 μm to Ra=4.03 μm. It is found that steady-state CHF increases with
increase in the Ra. Improved wettability and increased nucleation site density resulted
in the CHF enhancement by rough surface. The microchannel geometries namely,
square (SM-1.0), parabolic (PM-1.6) and stepped (SM-1.6) were fabricated by VMC
machining. The improved liquid supply through the channel space and significant
bubble growth resulted in the CHF enhancement by the microchannel geometry. The
CHF enhancement by SM-1.6 is highest among all the microchannel geometries.
The experimental setup is commissioned with programmable power supply to compare
the CHF of water during pool boiling on rough surface and microchannel geometry
under steady-state and exponential heat supply. The time constant (γ) of exponential
heat supply is varied from 1 to 6. It is found that both, rough surfaces and microchannel
geometries enhance the transient CHF. However, transient CHF gradually decreasedwith increase in γ due to liquid-vapor instability during exponential heat supply. CHF
increased with increase in the pressure at both the condition viz. steady and transient.
Steady-state CHF for Ra=4.03 μm and SM-1.6 at P=10 bar is found to be 71.43% and
47.37% higher compared to the CHF at P=1 bar, respectively.
The correlation for heat transfer coefficient is developed for prediction of transient
boiling performance which includes the non-dimensional time constant γ. Present
correlation predicts the experimental values of transient HTC with MAE of 14.91%.
CHF model for rough surface, based on force balance approach, is developed
incorporating the effect of time constant, bubble angle and roughness parameter viz.
Ra, Sm to predict the boiling crisis during pool boiling. It predicts the experimental
transient CHF with MAE of 11.89%.
Boiling videos are recorded at 1000 fps using high speed camera during the experiments
to study the bubble dynamics during pool boiling on rough surface and microchannel
geometries upto 10 bar pressure. Bubble dynamics during pool boiling of saturated
water is significantly affected by the surface characteristics i.e. surface roughness and
microchannel. Prolonged nucleated boiling regime is noticed for rough surface at high
pressure due to the capillary wicking in the unidirectional scratches which retards the
horizontal coalescence. Forces acting vertically on the growing bubble are considered
to predict the bubble departure diameter. The MAE between measured and predicted
bubble departure diameter for the rough surface and microchannel geometries at all
pressure is 17.09% and 13.30%, respectively.
Description
Keywords
Department of Mechanical Engineering, critical heat flux, heat transfer coefficient, wettability, capillary wicking, bubble dynamics